ES2113836T3 - PROCEDURE FOR THE SELECTIVE HYDROGENATION OF HIGHLY SATURATED COMPOUNDS IN HYDROCARBON CURRENTS. - Google Patents

PROCEDURE FOR THE SELECTIVE HYDROGENATION OF HIGHLY SATURATED COMPOUNDS IN HYDROCARBON CURRENTS.

Info

Publication number
ES2113836T3
ES2113836T3 ES94924461T ES94924461T ES2113836T3 ES 2113836 T3 ES2113836 T3 ES 2113836T3 ES 94924461 T ES94924461 T ES 94924461T ES 94924461 T ES94924461 T ES 94924461T ES 2113836 T3 ES2113836 T3 ES 2113836T3
Authority
ES
Spain
Prior art keywords
current
catalysting
milk
hydrogenation
selective hydrogenation
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
ES94924461T
Other languages
Spanish (es)
Other versions
ES2113836T1 (en
Inventor
Dennis Hearn
Robert P Arganbright
Edward M Jones Jr
Lawrence A Smith Jr
Gary R Gildert
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Chemical Research and Licensing Co
Original Assignee
Chemical Research and Licensing Co
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Chemical Research and Licensing Co filed Critical Chemical Research and Licensing Co
Publication of ES2113836T1 publication Critical patent/ES2113836T1/en
Application granted granted Critical
Publication of ES2113836T3 publication Critical patent/ES2113836T3/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G70/00—Working-up undefined normally gaseous mixtures obtained by processes covered by groups C10G9/00, C10G11/00, C10G15/00, C10G47/00, C10G51/00
    • C10G70/02—Working-up undefined normally gaseous mixtures obtained by processes covered by groups C10G9/00, C10G11/00, C10G15/00, C10G47/00, C10G51/00 by hydrogenation
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C5/00—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms
    • C07C5/02—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by hydrogenation
    • C07C5/03—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by hydrogenation of non-aromatic carbon-to-carbon double bonds
    • C07C5/05—Partial hydrogenation
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G45/00—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds
    • C10G45/32—Selective hydrogenation of the diolefin or acetylene compounds

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)

Abstract

UN PROCESO PARA LA HIDROGENACION SELECTIVA DE DIOLEFINAS Y COMPUESTOS ACETILENICOS EN UNA CORRIENTE DE HIDROCARBURO ALIFATICO RICA EN OLEFINA (1) COMPRENDE LA PUESTA EN CONTACTO DE LA CORRIENTE DE ALIMENTACION (1) A 40-300 (GRADOS) F BAJO PRESION PARCIAL DE HIDROGENO BAJO DE 0,1-70 PSIA A UNA PRESION TOTAL DE 0-350 PSIG EN UN REACTOR DE COLUMNA DE DESTILACION (10) QUE CONTIENE UN LECHO CATALIZADOR DE HIDROGENACION (12) QUE SIRVE COMO UN COMPONENTE DE UNA ESTRUCTURA DE DESTILACION (10), TAL Y COMO SOPORTA PDO ENCERRADO EN UNA REJILLA DE HILO METALICO TUBULAR. ESENCIALMENTE NO SE PRODUCE LA HIDROGENACION DE OLEFINAS. LA CORRIENTE DE ALIMENTACION (1) SE INTRODUCE POR DEBAJO O EN EL EXTREMO INFERIOR DEL LECHO CATALIZADOR (12), Y SE PONE EN CONTACTO CON HIDROGENO ALIMENTADO A TRAVES DE UN CIRCUITO (2) EN EL LECHO CATALIZADOR (12). LA PARTE SUPERIOR (3) SE OBTIENE EN LA PARTE SUPERIOR, CONDENSADA EN UN CONDENSADOR (20) Y SEPARADA EN UN ASENTADOR (30), Y PARCIALMENTE RECICLADA COMO UN LECHO CATALIZADOR (12) COMO UNA CORRIENTE DE REFLUJO (6). LA CORRIENTE INFERIOR (11) SE OBTIENE EN EL EXTREMO INFERIOR DEL REACTOR DE DESTILADO, Y ES PARCIALMENTE RECICLADA COMO UNA CORRIENTE (4) DESPUES DE SER CALENTADA EN UN INTERCAMBIADOR DE CALOR (40) COMO UNA CORRIENTE DE RECICLADO (13). EL EFLUENTE DE HIDROGENACION NETO SE OBTIENE COMO UNA CORRIENTE (9), Y GASES LIGEROS COMO CORRIENTE (7).A PROCESS FOR THE SELECTIVE HYDROGENATION OF DIOLEFINES AND ACETYLENE COMPOUNDS IN A CORRIENT OF ALIFATICO HYDROCARBON RICH IN OLEFINA (1) UNDERSTANDS THE COMMISSIONING OF THE POWER SUPPLY (1) TO 40-300 BAION GRADE FROM 0.1-70 PSIA TO A TOTAL PRESSURE OF 0-350 PSIG IN A DISTILLATION COLUMN REACTOR (10) CONTAINING A HYDROGENIZATION CATALYSTING MILK (12) THAT SERVES AS A COMPONENT OF A DISTILLATION STRUCTURE (10), AS AND AS SUPPORT PDO CLOSED IN A TUBULAR METAL THREAD GRILLE. ESSENTIALLY NO HYDROGENATION OF OLEFINS IS PRODUCED. THE POWER SUPPLY CURRENT (1) IS INTRODUCED BELOW OR IN THE LOWER END OF THE CATALYSTING MILK (12), AND IS CONTACTED WITH HYDROGEN FEEDED THROUGH A CIRCUIT (2) IN THE CATALYSTING MILK (12). THE UPPER PART (3) IS OBTAINED IN THE UPPER PART, CONDENSED IN A CONDENSER (20) AND SEPARATED IN A SETTLER (30), AND PARTIALLY RECYCLED AS A CATALYSTING MILK (12) AS A REFLUX CURRENT (6). THE LOWER CURRENT (11) IS OBTAINED AT THE LOWER END OF THE DISTILLED REACTOR, AND IS PARTIALLY RECYCLED AS A CURRENT (4) AFTER HEATING IN A HEAT EXCHANGER (40) AS A RECYCLING CURRENT (13). THE NET HYDROGENATION EFFLUENT IS OBTAINED AS A CURRENT (9), AND LIGHT GASES AS A CURRENT (7).

ES94924461T 1993-12-08 1994-07-21 PROCEDURE FOR THE SELECTIVE HYDROGENATION OF HIGHLY SATURATED COMPOUNDS IN HYDROCARBON CURRENTS. Expired - Lifetime ES2113836T3 (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US16331193A 1993-12-08 1993-12-08

Publications (2)

Publication Number Publication Date
ES2113836T1 ES2113836T1 (en) 1998-05-16
ES2113836T3 true ES2113836T3 (en) 2002-03-01

Family

ID=22589446

Family Applications (1)

Application Number Title Priority Date Filing Date
ES94924461T Expired - Lifetime ES2113836T3 (en) 1993-12-08 1994-07-21 PROCEDURE FOR THE SELECTIVE HYDROGENATION OF HIGHLY SATURATED COMPOUNDS IN HYDROCARBON CURRENTS.

Country Status (20)

Country Link
EP (1) EP0733030B1 (en)
JP (1) JP3621104B2 (en)
KR (1) KR960706461A (en)
CN (1) CN100343206C (en)
AU (1) AU682385B2 (en)
CA (1) CA2178612C (en)
CZ (1) CZ297855B6 (en)
DE (2) DE69428911T2 (en)
ES (1) ES2113836T3 (en)
FI (1) FI962401A (en)
MY (1) MY111451A (en)
NO (1) NO317488B1 (en)
OA (1) OA10364A (en)
PL (1) PL192732B1 (en)
PT (1) PT733030E (en)
RU (1) RU2145952C1 (en)
SA (1) SA94150351B1 (en)
TW (1) TW265333B (en)
WO (1) WO1995015934A1 (en)
ZA (1) ZA945342B (en)

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US5679241A (en) * 1995-05-17 1997-10-21 Abb Lummus Global Inc. Olefin plant recovery system employing catalytic distillation
US5689013A (en) * 1995-09-12 1997-11-18 Neste Ot Process for preparing tertiary alkyl ethers from an olefinic hydrocarbon feedstock
US5925799A (en) * 1996-03-12 1999-07-20 Abb Lummus Global Inc. Catalytic distillation and hydrogenation of heavy unsaturates in an olefins plant
AU2273597A (en) * 1996-03-12 1997-10-01 Abb Lummus Global Inc. Catalytic distillation and hydrogenation of heavy unsaturates in an olefins plant
AU2818197A (en) * 1996-08-15 1998-03-06 Catalytic Distillation Technologies Process for the production of mtbe
DE19636064A1 (en) * 1996-09-05 1998-03-12 Basf Ag Hydrogenation process
US5877363A (en) * 1996-09-23 1999-03-02 Catalytic Distillation Technologies Process for concurrent selective hydrogenation of acetylenes and 1,2 butadine in hydrocarbon streams
BR0007568B1 (en) * 1999-01-21 2010-11-16 process for selective hydrogenation of an impurity in a hydrocarbon-containing filler.
US6090270A (en) * 1999-01-22 2000-07-18 Catalytic Distillation Technologies Integrated pyrolysis gasoline treatment process
FR2806093B1 (en) 2000-03-08 2002-05-03 Inst Francais Du Petrole SELECTIVE HYDROGENATION PROCESS COMPRISING A PARTIAL SEPARATION OF HYDROGEN BY MEMBRANE UPSTREAM OF A REACTIVE COLUMN
US6414205B1 (en) 2000-03-24 2002-07-02 Catalytic Distillation Technologies Process for the removal of MAPD from hydrocarbon streams
US6759562B2 (en) * 2002-07-24 2004-07-06 Abb Lummus Global Inc. Olefin plant recovery system employing a combination of catalytic distillation and fixed bed catalytic steps
US6734328B1 (en) 2002-11-08 2004-05-11 Catalytic Distillation Technologies Process for the selective hydrogenation of alkynes
FR2850664B1 (en) * 2003-01-31 2006-06-30 Inst Francais Du Petrole SELECTIVE HYDROGENATION PROCESS USING A CATALYTIC REACTOR WITH SELECTIVE HYDROGEN MEMBRANE
US7045669B2 (en) 2003-08-05 2006-05-16 Catalytic Distillation Technologies Dual pressure catalytic distillation hydrogenation column system for the front end of an ethylene plant
WO2005080530A1 (en) * 2004-01-20 2005-09-01 Abb Lummus Global Inc. Improved olefin plant recovery system employing a combination of catalytic distillation and fixed bed catalytic steps
US7208646B2 (en) 2004-05-14 2007-04-24 Catalytic Distillation Technologies Selective hydrogenation of butadiene
US20060173224A1 (en) 2005-02-01 2006-08-03 Catalytic Distillation Technologies Process and catalyst for selective hydrogenation of dienes and acetylenes
FR2927267B1 (en) * 2008-02-07 2010-04-16 Inst Francais Du Petrole SELECTIVE HYDROGENATION CATALYST AND PROCESS FOR PREPARING THE SAME
CN102666807B (en) 2009-11-10 2016-01-20 国际壳牌研究有限公司 For the production of the method for alkene
EP2499219A2 (en) 2009-11-10 2012-09-19 Shell Internationale Research Maatschappij B.V. Process for producing olefins
AU2010318050B2 (en) 2009-11-10 2013-12-12 Shell Internationale Research Maatschappij B.V. Process and integrated system for the preparation of a lower olefin product
SG10201407378RA (en) 2009-11-10 2015-01-29 Shell Int Research Process for the preparation of a lower olefin product
CA2779260A1 (en) 2009-11-10 2011-05-19 Shell Internationale Research Maatschappij B.V. Process for producing ethylene oxide
US9707530B2 (en) 2012-08-21 2017-07-18 Uop Llc Methane conversion apparatus and process using a supersonic flow reactor
US9205398B2 (en) 2012-08-21 2015-12-08 Uop Llc Production of butanediol from a methane conversion process
US20140058145A1 (en) * 2012-08-21 2014-02-27 Uop Llc Production of olefins from a methane conversion process
US9327265B2 (en) 2012-08-21 2016-05-03 Uop Llc Production of aromatics from a methane conversion process
US9689615B2 (en) 2012-08-21 2017-06-27 Uop Llc Steady state high temperature reactor
US9370757B2 (en) 2012-08-21 2016-06-21 Uop Llc Pyrolytic reactor
US9308513B2 (en) 2012-08-21 2016-04-12 Uop Llc Production of vinyl chloride from a methane conversion process
US9434663B2 (en) 2012-08-21 2016-09-06 Uop Llc Glycols removal and methane conversion process using a supersonic flow reactor
US8933275B2 (en) 2012-08-21 2015-01-13 Uop Llc Production of oxygenates from a methane conversion process
US8927769B2 (en) 2012-08-21 2015-01-06 Uop Llc Production of acrylic acid from a methane conversion process
US20140058149A1 (en) * 2012-08-21 2014-02-27 Uop Llc High efficiency processes for olefins, alkynes, and hydrogen co-production from light hydrocarbons such as methane
US9023255B2 (en) 2012-08-21 2015-05-05 Uop Llc Production of nitrogen compounds from a methane conversion process
US9656229B2 (en) 2012-08-21 2017-05-23 Uop Llc Methane conversion apparatus and process using a supersonic flow reactor
US8937186B2 (en) 2012-08-21 2015-01-20 Uop Llc Acids removal and methane conversion process using a supersonic flow reactor
US9822317B2 (en) * 2014-10-10 2017-11-21 Uop Llc Process and apparatus for selectively hydrogenating naphtha
CN106582636B (en) * 2015-10-14 2019-04-12 中国石油化工股份有限公司 Composite catalyst bed
CN107573239B (en) * 2016-07-05 2021-02-12 中国石油化工股份有限公司 Synthetic method of tert-amyl acetate
KR20200072540A (en) 2017-10-25 2020-06-22 바스프 에스이 Method for removing diene from a material stream comprising C3 to C5 hydrocarbons by selective hydrogenation

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GB835689A (en) * 1957-12-17 1960-05-25 Bayer Ag Process for removing acetylene, methyl acetylene, and allene from hydrocarbon mixtures
DE1958449A1 (en) * 1968-12-17 1970-07-02 Leuna Werke Veb Selective hydrogenation of acetylene hydro - carbons in olefine fractions
DD131644B1 (en) * 1977-06-01 1980-02-13 Eberhard Grasshoff METHOD FOR THE SELECTIVE HYDROGENATION OF C TWO MINUS FRACTIONS
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US4215011A (en) * 1979-02-21 1980-07-29 Chemical Research And Licensing Company Catalyst system for separating isobutene from C4 streams
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DD150312A3 (en) * 1979-04-18 1981-08-26 Siegfried Queck METHOD FOR SELECTIVE HYDROGENATION OF FLOW NOZZLES 3-FRACTIONS
CS219725B1 (en) * 1981-01-04 1983-03-25 Jaromir Vybihal Method of preparation of the butene -1 from the butene fraction
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US5087780A (en) * 1988-10-31 1992-02-11 Chemical Research & Licensing Company Hydroisomerization process
AU654757B2 (en) * 1992-02-10 1994-11-17 Chemical Research & Licensing Company Selective hydrogenation of C5 streams

Also Published As

Publication number Publication date
SA94150351B1 (en) 2005-10-16
JPH09511261A (en) 1997-11-11
TW265333B (en) 1995-12-11
WO1995015934A1 (en) 1995-06-15
CZ169996A3 (en) 1997-02-12
KR960706461A (en) 1996-12-09
CA2178612A1 (en) 1995-06-15
JP3621104B2 (en) 2005-02-16
DE69428911D1 (en) 2001-12-06
EP0733030A4 (en) 1998-03-04
OA10364A (en) 2001-11-16
CZ297855B6 (en) 2007-04-18
CN100343206C (en) 2007-10-17
PL314964A1 (en) 1996-09-30
NO317488B1 (en) 2004-11-08
CN1141622A (en) 1997-01-29
PT733030E (en) 2002-02-28
DE69428911T2 (en) 2002-06-06
EP0733030B1 (en) 2001-10-31
MY111451A (en) 2000-05-31
FI962401A0 (en) 1996-06-10
AU7472094A (en) 1995-06-27
NO962442D0 (en) 1996-06-10
ES2113836T1 (en) 1998-05-16
FI962401A (en) 1996-07-24
CA2178612C (en) 2002-10-01
NO962442L (en) 1996-08-05
PL192732B1 (en) 2006-12-29
RU2145952C1 (en) 2000-02-27
EP0733030A1 (en) 1996-09-25
ZA945342B (en) 1995-03-01
AU682385B2 (en) 1997-10-02
DE733030T1 (en) 1997-02-13

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